WO2003024396A2 - Dry powder medicament formulations - Google Patents

Dry powder medicament formulations Download PDF

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Publication number
WO2003024396A2
WO2003024396A2 PCT/US2002/029267 US0229267W WO03024396A2 WO 2003024396 A2 WO2003024396 A2 WO 2003024396A2 US 0229267 W US0229267 W US 0229267W WO 03024396 A2 WO03024396 A2 WO 03024396A2
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WO
WIPO (PCT)
Prior art keywords
excipient
pharmaceutical composition
particles
medicament
respirable
Prior art date
Application number
PCT/US2002/029267
Other languages
English (en)
French (fr)
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WO2003024396A3 (en
Inventor
Andrew Bruce Brown
Michael Mary Van Oort
Original Assignee
Glaxo Group Limited
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Glaxo Group Limited filed Critical Glaxo Group Limited
Priority to JP2003528494A priority Critical patent/JP2005507881A/ja
Priority to US10/489,491 priority patent/US8337816B2/en
Priority to EP02798971A priority patent/EP1487417A4/en
Priority to AU2002333644A priority patent/AU2002333644A1/en
Publication of WO2003024396A2 publication Critical patent/WO2003024396A2/en
Publication of WO2003024396A3 publication Critical patent/WO2003024396A3/en

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Classifications

    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/0012—Galenical forms characterised by the site of application
    • A61K9/007—Pulmonary tract; Aromatherapy
    • A61K9/0073—Sprays or powders for inhalation; Aerolised or nebulised preparations generated by other means than thermal energy
    • A61K9/0075—Sprays or powders for inhalation; Aerolised or nebulised preparations generated by other means than thermal energy for inhalation via a dry powder inhaler [DPI], e.g. comprising micronized drug mixed with lactose carrier particles
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/141—Intimate drug-carrier mixtures characterised by the carrier, e.g. ordered mixtures, adsorbates, solid solutions, eutectica, co-dried, co-solubilised, co-kneaded, co-milled, co-ground products, co-precipitates, co-evaporates, co-extrudates, co-melts; Drug nanoparticles with adsorbed surface modifiers
    • A61K9/145—Intimate drug-carrier mixtures characterised by the carrier, e.g. ordered mixtures, adsorbates, solid solutions, eutectica, co-dried, co-solubilised, co-kneaded, co-milled, co-ground products, co-precipitates, co-evaporates, co-extrudates, co-melts; Drug nanoparticles with adsorbed surface modifiers with organic compounds
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P11/00—Drugs for disorders of the respiratory system
    • A61P11/08—Bronchodilators
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P29/00—Non-central analgesic, antipyretic or antiinflammatory agents, e.g. antirheumatic agents; Non-steroidal antiinflammatory drugs [NSAID]
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P37/00—Drugs for immunological or allergic disorders
    • A61P37/08—Antiallergic agents
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/1605—Excipients; Inactive ingredients
    • A61K9/1629—Organic macromolecular compounds
    • A61K9/1652—Polysaccharides, e.g. alginate, cellulose derivatives; Cyclodextrin

Definitions

  • the present invention relates generally to pharmaceutical compositions. More particularly, the invention relates to inhalable dry powder medicament formulations and pharmaceutical compositions for delivery of one or more medicaments to the pulmonary system.
  • compositions may advantageously be administered by inhalation to or through the lung of a patient.
  • a pharmaceutical delivery device such as a dry powder inhaler ("DPI")
  • DPI dry powder inhaler
  • a dose of the pharmaceutical composition is positioned in an aerosolization chamber, where it is aerosolized and, hence, dispersed into respirable particles by airflow supplied by a pressurized source of gas or by the patient's inspiration effort.
  • the dispersed particles must be of suitable size.
  • the pulmonary system includes the upper airways, including the oropharynx and larynx, followed by the lower airways, which include the trachea followed by bifurcations into bronchi and bronchioli.
  • the upper and lower airways are called the conducting airways.
  • the terminal bronchioli then divide into respiratory bronchioli, which then lead to the alveolar region, or the deep lung. See, Gonda, I, "Aerosols for Delivery of
  • the smooth muscle regions of the conducting airways, and particularly the lower airways possess receptors (i.e., protein based, macromolecular complexes existing within cell membranes which, upon interaction with specific agents, change conformation and lead to the triggering of a cellular response, such as smooth muscle cell contraction or relaxation) that are the primary target site of local medicament particle delivery.
  • receptors i.e., protein based, macromolecular complexes existing within cell membranes which, upon interaction with specific agents, change conformation and lead to the triggering of a cellular response, such as smooth muscle cell contraction or relaxation
  • the alveolar region of the deep lung although it too may possess receptors effecting local response, is the target site for pulmonary systemic delivery, as the alveoli provide access to vascular system through a closely associated vascular capillary network.
  • medicament particles deposit in specific areas of the pulmonary system based upon the aerodynamic size of the particles and the flow rate of the fluid within which they are entrained.
  • particles having an aerodynamic diameter in the range of 0.5 to 3 ⁇ m are suitable for systemic delivery, as these particles deposit selectively in the deep lung.
  • Particles having an aerodynamic diameter in the range of approximately 0.5 to 10 ⁇ m, preferably, 1 to 6 ⁇ m, and more preferably, 3 to 6 ⁇ m are suitable for local lung delivery, as they will deposit in the conductive airways.
  • Particles having an aerodynamic diameter greater than 10 ⁇ m generally deposit in the mouth, throat or upper airways, offering little therapeutic benefit. Particles having an aerodynamic diameter less than 0.5 ⁇ m do not settle out of the air flow to deposit in the lungs, and are subsequently respired when the patient exhales.
  • the effectiveness of dry powder pharmaceutical composition delivery depends upon the ability to precisely and reproducibly meter small quantities of medicament into doses. The metering is typically achieved by diluting the medicament in a pharmaceutical composition containing one or more excipients. The pharmaceutical composition can then be metered with a greater margin of error than a highly potent medicament alone.
  • the pharmaceutical composition should be sufficiently flowable to permit the composition to be poured or otherwise transferred into individual doses.
  • Measures of flowability are typically quantified by the compressibility of the powder composition, as well as its "angle of repose.” Measurement of these features may be made using standardized methodologies known in the art.
  • Compositions are also advantageously highly aerosolizable, to clear the composition from the inhaler device.
  • the composition is preferably dispersible into particles of respirable size. Measurements of aerosolizibility and dispersiblity may be made by measuring the emitted dose and fine particle fraction of the composition, respectively, using methodologies known to the art.
  • a common device used in measuring fine particle fraction is an Anderson Cascade Impactor.
  • an excipient powder for use with an inhalable micronized medicament that has coarse and fine excipient fractions.
  • the coarse fraction improves aerosolibility (i.e., emitted dose), while the fine fraction improves dispersability (i.e., measured as fine particle fraction).
  • the coarse excipient fraction i.e., mill ground
  • the fine excipient fraction has an average particle size no greater than 10 ⁇ m.
  • the medicament has a particle size no greater than 10 ⁇ m.
  • an excipient powder comprising a coarse first fraction of which at least 80% by weight has a particle size of at least 10 ⁇ m; a fine second fraction which at least 90% by weight has a particle size of no greater than 10 ⁇ m; and a third fraction consisting of a ternary agent.
  • the ternary agent is provided in an additional fine (i.e., 10 ⁇ m or less) fraction, but slightly larger sizes are acceptable.
  • the disclosed suitable ternary agents include water soluble and physiologically acceptable materials, i.e., water surface active or amino acids, peptides and polypeptides or derivatives thereof, with the preferred ternary agent being L-leucine.
  • particles with a diameter in the range of 10 to 30 ⁇ m have an adverse effect on powder flow characteristics without imparting any benefit of medicament delivery (i.e., dispersion).
  • respirable engineered particle compositions have morphologies and physical and chemical attributes with allegedly superior aerodynamic characteristics. These particles may be hollow or porous, and have a range of particle densities, all providing better aerosolization characteristics.
  • prior art compositions containing milled respirable drug particles and large excipient carrier particle systems may allow for at least some medicament particles to loosely bind to the surface of the large carrier surface and disengage upon inhalation, but a substantial amount of the medicament fails to disengage from the large lactose particles and is deposited in the throat.
  • PCT Patent Publication WO 99/16419 discloses microporous microparticles containing a medicament, an excipient (i.e., lactose) and surfactant.
  • lactose lactose
  • surfactant i.e., lactose
  • the microporous nature of these particles purportedly provides superior aerodynamic characteristics, allowing particle-to-particle aggregation to be overcome without the use of large excipient particles. This advance allows the large excipient carriers particles to be eliminated from the formulation altogether.
  • U.S. Pat. No. 5,993,805 discloses smooth, spherical, solid walled, hollow microparticles (1 to lO ⁇ m in size) that are intended for aerosolized medicament delivery to the lung(s). This reference similarly does not address the use of large excipient particles.
  • U.S. Pat. Nos. 5,874,064, 5,855,913 and 5,985,309 which are incorporated by reference herein, disclose low density particle compositions that can be readily entrained into the inhalation path of a patient and deposited into the desired areas of the lungs of a patient to effectuate local or systemic delivery.
  • the particle compositions have a tap density less than 0.4 g/cm 3 and a mass mean diameter in the range of 5 to 30 ⁇ m to yield an aerodynamic diameter of 1 to 5 ⁇ m.
  • the medicament is adsorbed, absorbed, or otherwise incorporated onto or into the matrix of low-density particles.
  • these low-density particles are deliverable with larger carrier particles having no medicament, but a mean diameter in the range of 50 to 100 ⁇ m. No other mention is made of attributes of the large carrier particles in question.
  • Progress in the art of dry powder pharmaceutical compositions, in terms of meterability, flowability, dispersiblity and aerosolibility remains desirable.
  • Micronized medicament/excipient blends are encumbered to a certain degree by their inherent aerodynamic attributes. Thus, achieving very high degrees of aerosolibility and dispersiblity using micronized excipients is somewhat limited by these attributes. Modification of the physical structure of the particles incorporating the medicament or bioactive agent via particle engineering is also often difficult or impossible due to the physical and chemical properties of the active agent itself. Indeed, it is well known that not all medicaments (or bioactive agents) can be incorporated in a particle matrix to provide desired aerodynamic properties suitable for inhalation. Limitations also exist in the ability to incorporate specific concentrations,, such as very high or low concentrations, of certain medicaments into suitable matrix forms.
  • the dry powder pharmaceutical composition in accordance with this invention generally comprises (i) a medicament fraction comprising medicament particles with an aerodynamic diameter no greater than 10 ⁇ m; and (ii) at least 50% of a non-respirable excipient fraction comprising excipient particles with an aerodynamic diameter greater than 10 ⁇ m and a geometric diameter greater than 30 ⁇ m.
  • the pharmaceutical composition includes a respirable excipient fraction comprising excipient particles with an aerodynamic diameter no greater than 10 ⁇ m.
  • the non-respirable excipient particles have sufficient porosity (i.e., defining pores) to receive a portion of the respirable excipient fraction and/or the medicament fraction.
  • FIGURE 1 is an electron micrograph (i.e., SEM) of a porous non-respirable particle according to the invention
  • FIGURE 2 is an electron micrograph of a porous non-respirable particle having respirable particles disposed in defining pores of the non-respirable particle according to the invention.
  • FIGURE 3 is a graphical illustration of the effects of fines content on the fine particle mass (FPM) performance according to the invention.
  • medicament is meant to mean and include any substance (i.e., compound or composition of matter) which, when administered to an orgamsm (human or animal) induces a desired pharmacologic and or physiologic effect by local and/or systemic action.
  • biopharmaceuticals e.g., peptides, hormones, nucleic acids, gene constructs, etc.
  • analgesics e.g., codeine, dihydromorphine, ergotamine, fentanyl or morphine
  • anginal preparations e.g., diltiazem
  • antiallergics e.g., cromoglycate (e.g., as the sodium salt), ketotifen or nedocromil (e.g., as the sodium salt)
  • antiinfectives e.g., cephalosporins, penicillins, streptomycin, sulphonamides, tetracyclines and pentamidine
  • antihistamines e.g., methapyrilene
  • anti- inflammatories e.g., beclomethasone (e.g.
  • bromide as bromide
  • tiotropium as bromide
  • atropine or oxitropium hormones, e.g., cortisone, hydrocortisone or prednisolone
  • xanthines e.g., aminophylline, choline theophyllinate, lysine theophyllinate or theophylline
  • therapeutic proteins and peptides e.g., insulin or glucagon.
  • the noted medicaments may also be employed in the form of salts, (e.g., as alkali metal or amine salts or as acid addition salts) or as esters (e.g., lower alkyl esters) or as solvates (e.g., hydrates) to optimize the activity and/or stability of the medicament.
  • salts e.g., as alkali metal or amine salts or as acid addition salts
  • esters e.g., lower alkyl esters
  • solvates e.g., hydrates
  • the term “medicament” further includes formulations containing combinations of active ingredients, including, but not limited to, salbutamol (e.g., as the free base or the sulfate salt) or salmeterol (e.g., as the xinafoate salt) or formoterol (e.g., as the fumarate salt) in combination with an anti-inflammatory steroid such as a beclomethasone ester (e.g., the dipropionate), a fluticasone ester (e.g., the propionate), a furoate ester or budesonide.
  • an anti-inflammatory steroid such as a beclomethasone ester (e.g., the dipropionate), a fluticasone ester (e.g., the propionate), a furoate ester or budesonide.
  • medicament formulation and “pharmaceutical composition”
  • pharmaceutical composition it is meant to mean a combination of at least one medicament and one or more added components or elements, such as an “excipient” or “carrier.”
  • excipient and “carrier” generally refer to substantially inert materials that are nontoxic and do not interact with other components of the composition in a deleterious manner.
  • excipients include pharmaceutical grades of carbohydrates including monosaccharides, disaccharides, cyclodextrins and polysaccharides (e.g., dextrose, sucrose, lactose, raffinose, mannitol, sorbitol, irositol, dextrins and maltodextrins); starch; cellulose; salts (e.g., sodium or calcium phosphates, calcium sulfate, magnesium sulfate); citric acid; tartaric acid; glycine; leucine; high molecular weight polyethylene glyols (PEG); pluronics; surfactants; lubricants; stearates and their salts or esters (e.g., magnesium stearate, calcium stearate); amino acids; fatty acids; and combinations thereof.
  • suitable “carriers” include water, silicone, gelatin, waxes, and like materials.
  • D 50 as used herein, it is meant to mean the average geometric diameter (i.e., particle size).
  • pharmaceutical delivery device it is meant to mean a device that is adapted to administer a controlled amount of a composition to a patient, including, but not limited to, the Diskus® device disclosed in U.S. Pat Nos. Des. 342,994;
  • the present invention substantially reduces or eliminates the disadvantages and drawbacks associated with conventional dry powder pharmaceutical compositions and methods for producing same.
  • the unique pharmaceutical compositions can be readily employed to provide controlled systemic or local medicament delivery to the pulmonary system via aerosolization.
  • the pharmaceutical compositions include a medicament fraction and at least 50% of a non-respirable excipient fraction.
  • the medicament fraction preferably comprises medicament particles having an aerodynamic diameter no greater than 10 ⁇ m.
  • the non-respirable excipient fraction preferably comprises excipient particles having an aerodynamic diameter greater than 10 ⁇ m and a geometric diameter greater than 30 ⁇ m.
  • the non-respirable excipient particles are also preferably "low density.”
  • low density as used herein, it is meant to mean particles having a density less than 1 g/cm 3 .
  • the non-respirable excipient particles have a tap density less than 0.8 g/cm .
  • the non-respirable excipient particles have a tap density in the range of approximately 0.4 - 0.8 g/cm 3 .
  • the pharmaceutical compositions include a respirable excipient fraction comprising excipient particles with an aerodynamic diameter no greater than 10 ⁇ m.
  • the non- respirable excipient particles 5 have sufficient porosity (i.e., "defining pores", designated 6 in Fig. 1) to receive a portion of the respirable excipient fraction and/or the medicament fraction (designated generally 7 in Fig. 2).
  • the non-respirable excipient particles may contain fissures that are adapted, similar to the depicted porous particles, to releasably receive a portion of the respirable excipient fraction and/or medicament fraction.
  • the non-respirable excipient particles may be solid walled, with a smooth or dimpled exterior surface, and may contain an internal void
  • the medicament fraction and optionally, the respirable excipient fraction may be releasably carried on the external surface of the carrier.
  • the unique pharmaceutical compositions of the invention provide major advantages over comparable formulations. Among the advantages are enhanced FPM performance, flow characteristics and stability.
  • the medicament concentration and fill weight can also be selected to deliver the desired amount of medicament to the lung.
  • various features of the excipient particles such as surface texture and porosity, directly contribute to the aforementioned advantages. For example, it is well known that porous particles with a relatively large geometric diameter are particularly suitable for inhalation therapy. Due to their relatively large geometric diameter, porous particles exhibit better flow characteristics. Porous particles also have a much higher specific surface area than non-porous particles. Thus, dissolution of the medicament from such particles is faster than from non-porous particles.
  • porous excipient particles can readily be produced such that the porous particles have sufficient porosity to receive a portion of the respirable (i.e., micronized) excipient fraction or medicament fraction (see Fig. 2). As illustrated in Fig. 3, the use of such excipient particles allows a greater percentage of respirable excipient particles (i.e., fines) to be employed (in a low shear blending operation), resulting in enhanced FPM performance without adverse impact on the flow characteristics.
  • respirable excipient particles i.e., fines
  • the medicament fraction comprises at least one of the aforementioned medicaments.
  • the medicament fraction comprises at least one of the following medicaments: codeine, dihydromorphine, ergotamine, fentanyl, morphine, diltiazem, cromoglycate, ketotifen, nedocromil; cephalosporins, penicillins, streptomycin, sulphona ides, tetracyclines pentamidine; methapyrilene, beclomethasone, fluticasone, flunisolide, budesonide, rofleponide, mometasone, ciclesonide, triamcinolone, noscapine, albuterol, salmeterol, ephedrine, adrenaline, fenoterol, formoterol, isoprenaline, metaproterenol, phenylephrine, phenylpropanolamine, pirbuterol,
  • the medicament fraction most preferably comprises fluticasone, fluticasone propionate or fluticasone furoate.
  • the medicament fraction comprises salmeterol or salmeterol xinafoate.
  • the medicament fraction comprises albuterol base or sulfate.
  • the medicament fraction comprises a combination of active ingredients, including, but not limited to, salmeterol, salmeterol xinafoate, or albuterol base (or sulfate) in combination with fluticasone propionate or fluticasone furoate.
  • active ingredients including, but not limited to, salmeterol, salmeterol xinafoate, or albuterol base (or sulfate) in combination with fluticasone propionate or fluticasone furoate.
  • the medicament fraction comprises medicament particles coated or co-precipitated with an additional excipient, by any suitable means.
  • the additional excipient can be a surfactant, lubricant, polymer, amino acid, DPPC, polylactide, polysaccharide, targeting material, material having an opposite charge from the medicament, or any other material that provides beneficial properties to the aerosolibility, dispersability or therapeutic release profile of the medicament.
  • the medicament fraction is in the range of approximately 0.01 to 50%, preferably, 0.01 to 30%, more preferably, 0.01 to 20% by weight of the dry powder pharmaceutical composition. In a preferred embodiment of the invention, the medicament fraction is less than 10% by weight of the composition.
  • the medicament particles of the invention can be produced into appropriately sized particles by any suitable method of particle formation.
  • suitable methods include, but are not limited to, micronization, milling, spray drying and solvent/anti-solvent crystallization.
  • micronization or milling are employed to produce the particles of the invention.
  • the medicament particles of the invention preferably have an aerodynamic diameter no greater than 10 ⁇ m.
  • the diameter of the medicament particles will, in accordance with the invention, range depending on factors such as particle composition and methods of synthesis.
  • the medicament particles have an aerodynamic diameter in the range of approximately 0.5 to 6 ⁇ m. More preferably, the medicament particles have an aerodynamic diameter in the range of approximately 2 to 6 ⁇ m. For systemic delivery, the medicament particles preferably have an aerodynamic diameter in the range of approximately 0.5 to 3 ⁇ m.
  • the medicament particles have a geometric diameter in the range of approximately 5 to 30 ⁇ m, wherein the tap density of the medicament particles is less than approximately 0.4 g/cm 3 .
  • the noted particles have an aerodynamic diameter in the range of approximately 1 to 5 ⁇ m.
  • the tap density which has been used as a measure of the envelope mass density, is generally useful in characterizing the density of objects having irregular size and shape.
  • Envelope density is generally determined by dividing the mass of an object by its volume, where the volume includes that of its pores and small cavities, but excludes interstitial spaces.
  • the non-respirable excipient fraction comprises at least one of the aforementioned excipients.
  • the excipient is preferably biodegradable and biocompatible.
  • the non-respirable excipient fraction comprises at least one of the following excipients: pharmaceutical grades of carbohydrates (e.g., polysaccharides), amino acids, fatty acids, bio-compatible polymers or inorganic salts. More preferably, the non-reparable excipient fraction comprises lactose, mannitol, maltose, maltodextrins, dextrose, phenylalanine, leucine, glycine, diketopiperazine, calcium stearate, sodium stearyl fumarate, polylactic acid (PLA), polylactic-coglycolic acid (PLGA), a calcium salt and/or combinations thereof.
  • pharmaceutical grades of carbohydrates e.g., polysaccharides
  • amino acids amino acids
  • fatty acids fatty acids
  • bio-compatible polymers or inorganic salts More preferably, the non-reparable excipient fraction comprises lactose, mannitol, maltose, maltodextrins,
  • the excipient fraction comprises mannitol.
  • the non-respirable excipient fraction preferably comprises excipient particles having an aerodynamic diameter greater than approximately 10 ⁇ m and a geometric diameter greater than 30 ⁇ m.
  • the non-respirable excipient particles are also preferably low density (i.e., tap density less than 0.8 g/cm 3 ).
  • the non-respirable excipient particles have sufficient porosity (i.e., defining pores) to receive a portion of the medicament fraction and/or the respirable excipient fraction, discussed below.
  • the non- respirable excipient particles may be fissured or solid walled, but hollow.
  • the non-respirable excipient particles can be produced using any conventional methods known in the art.
  • the non-respirable excipient particles can also be fabricated or separated, for example by filtration, to provide a non-respirable excipient fraction with a preselected particle size distribution.
  • a preselected particle size distribution For example, greater than 30%, 50%, 70%, or 80% of the particles in the non-respirable excipient fraction can have geometric diameter of at least 50 ⁇ m.
  • the selected geometric diameter ranges within which a certain percentage of the non-respirable excipient particles must fall can be, for example, between about 30 to 300 ⁇ m, 60 to 160 ⁇ m, or 90 to 150 ⁇ m.
  • greater than 50%, more preferably, greater than 70% of the non-respirable excipient particles have a geometric diameter greater than 50 ⁇ m.
  • greater than 90% of the non-respirable excipient fraction have a geometric diameter in the range of approximately 30 to 300 ⁇ m.
  • the use of larger particles is advantageous since the larger particles are able to flow more efficiently than smaller, aerosol particles, such as those currently employed for inhalation therapies.
  • the presence of the higher proportion of the larger diameter particles in the non-respirable excipient fraction also enhances the delivery of the medicaments to the deep lung.
  • compositions of the present invention can be further enhanced through the addition of a respirable sized excipient fraction comprising excipient particles with an aerodynamic diameter of 10 ⁇ m or less. More preferably, the respirable excipient particles have an aerodynamic diameter in the range of approximately 1 to 7 ⁇ m.
  • the respirable excipient particles are similarly preferably biodegradable and biocompatible, and optionally are capable of biodegrading at a controlled rate for delivery of a medicament.
  • the respirable excipient particles can be formed of any excipient that is suitable for pulmonary delivery.
  • the excipient particles are formed by micronization or milling (i.e., wet or dry).
  • such particles can be formed by spray drying, spray freeze drying, or other suitable processes.
  • the respirable excipient fraction can comprise any suitable excipient (and combinations thereof) including, but not limited to, sugars, lubricants, fatty acids, amino acids, stearates and their salts or esters, calcium salts and derivatives thereof, and biocompatible polymers. More preferably, the respirable excipient fraction comprises mannitol, lactose, phenylalanine, glycine, leucine, dibasic calcium phosphate, tribasic calcium phosphate, polylactic acid (PLA), polylactic- coglycolic acid (PLGA), diketopiperazine, calcium stearate, sodium stearyl fumarate, magnesium stearate and/or combinations thereof.
  • suitable excipient including, but not limited to, sugars, lubricants, fatty acids, amino acids, stearates and their salts or esters, calcium salts and derivatives thereof, and biocompatible polymers. More preferably, the respirable excipient fraction comprises mannitol, lactose
  • the respirable excipient fraction (i.e., micronized fraction) comprises in the range of 5% to 50% by weight of the dry powder pharmaceutical composition. In a still further embodiment, it is preferred that greater than 50% of the respirable excipient particles have an aerodynamic diameter in the range of approximately 1 to 8 ⁇ m.
  • the pharmaceutical compositions in accordance with the invention can conveniently be filled into a bulk storage container, such as a multi-dose reservoir, or into unit dose containers such as capsules, cartridges or blister packs, which may be used with an appropriate pharmaceutical delivery device, for example, as described in GB 2041763, WO 91/13646, GB 1561835, GB 2064336, GB 2129691 or GB 2246299, which are incorporated by reference herein.
  • the noted devices and aforementioned pharmaceutical delivery devices, containing a pharmaceutical composition in accordance with the invention are deemed novel and, hence, form a further aspect of the invention.
  • compositions of the invention are particularly suitable for use with multi-dose reservoir-type devices in which the composition is metered, e.g., by volume from a bulk powder container into dose-metering cavities.
  • the lower limit of powder delivery which may be accurately metered from a multi-dose reservoir-type device, is typically in the range of 100 to 200 micrograms.
  • the pharmaceutical compositions of the present invention are therefore particularly advantageous for highly potent and, hence, low dose medicaments that require a high ratio of excipient for use in a multi-dose reservoir-type device.
  • Administration of the pharmaceutical compositions of the present invention may be appropriate for the treatment of mild, moderate or severe acute or chronic symptoms or for prophylactic treatment. It will be appreciated that the precise dose administered will depend on the age and condition of the patient, the particular medicament used and the frequency of administration and will ultimately be at the discretion of the attendant physician.
  • the invention includes the delivery of a dry powder pharmaceutical composition of the invention to the pulmonary system of a patient comprising: (i) providing a pharmaceutical delivery device containing a dry powder pharmaceutical composition comprising a medicament fraction and at least 50% of a non-respirable excipient fraction, the medicament fraction comprising medicament particles having an aerodynamic diameter no greater than 10 ⁇ m and the non- respirable excipient fraction comprising excipient particles having an aerodynamic diameter greater than 10 ⁇ m and a geometric diameter greater than 30 ⁇ m; (ii) introducing an air flow within said delivery device; (iii) aerosolizing the dry powder pharmaceutical composition into the air flow; (iv) dispersing the aerosolized pharmaceutical composition into a plume; (v) emitting the aerosolized pharmaceutical composition from the delivery device; and (vi) delivering the plume to the pulmonary system of the patient.
  • the delivery- device further comprises a source of aerosolization energy that is independent of patient inhalation effort.
  • the noted method further includes the step of releasing this aerosolization energy to create air flow which aerosolizes the dry powder pharmaceutical composition.
  • the dry powder pharmaceutical composition is emitted from the delivery device.
  • the fine particle fraction (e.g., medicament fraction) of the emitted dose is 40% or greater.
  • the invention further includes processes for forming the unique pharmaceutical compositions and the products produced thereby.
  • the process for forming the pharmaceutical compositions of the invention preferably comprises (i) providing medicament particles having an aerodynamic diameter no greater than 10 ⁇ m; (ii) providing first excipient particles having an aerodynamic diameter no greater than 10 ⁇ m; (iii) providing second excipient particles having an aerodynamic diameter greater than 10 ⁇ m and a geometric diameter greater than 30 ⁇ m; (iv) preblending the first and second excipient particles to form an excipient composition; and (v) blending the medicament particles and excipient composition.
  • the second excipient particles include defining pores. During the pre-blending step, a portion of the first excipient particles are disposed in the defining pores of the second excipient particles.
  • the process for forming the pharmaceutical compositions of the invention comprises (i) providing medicament particles having an aerodynamic diameter no greater than 10 ⁇ m; (ii) providing first excipient particles having an aerodynamic diameter no greater than 10 ⁇ m ; (iii) providing second excipient particles having an aerodynamic diameter greater than 10 ⁇ m and a geometric diameter greater than 30 ⁇ m; (iv) preblending the medicament particles and second excipient particles to form a medicament/excipient composition; and (v) blending the first excipient particles and medicament/excipient composition.
  • the second excipient particles include defining pores. During the pre-blending step, a portion of the medicament particles are disposed in the defining pores of the second excipient particles.
  • the process for forming the pharmaceutical compositions of the invention comprises (i) providing medicament particles having an aerodynamic diameter no greater than 10 ⁇ m; (ii) providing first excipient particles having an aerodynamic diameter no greater than 10 ⁇ m ; (iii) providing second excipient particles having an aerodynamic diameter greater than 10 ⁇ m and a geometric diameter greater than 30 ⁇ m; (iv) preblending the medicament particles and first excipient particles to form a medicament/excipient composition; and (v) blending the second excipient particles and medicament/excipient composition.
  • the second excipient particles include defining pores.
  • a portion of the medicament/excipient composition is disposed in the defining pores of the second excipient particles.
  • Pearlitol 200 spray dried mannitol - D 50 - 130-160 ⁇ m
  • Pearlitol 70 spray dried mannitol - D 50 - 65-90 ⁇ m
  • Each of the non-respirable excipients exhibited an aerodynamic diameter > 10 ⁇ m.
  • Respirable Excipients Spray dried glycine: D 50 - 6-8 ⁇ m
  • Tricalcium Phosphate D 50 - 5-7 ⁇ m
  • Preblending as used in the following examples, preblending entailed combining a coarse excipient fraction with a fine excipient or medicament fraction and blending in a low shear or high shear blending procedure for a given period of time, under specified conditions to achieve a homogenous first composition.
  • the preblending procedure employed comprised sandwiching the fine component between the two halves of coarse excipient and blending for 10 minutes at 90 rpm using a Turbula T2 blender (commercially available from. Glen Mills Inc., Clifton, NJ).
  • Blending as used in the following examples, blending entailed combining the homogeneous first composition with a further component (i.e., medicament or fine excipient) in a low shear or high shear blending procedure for a given period of time, under specified conditions to achieve a homogenous second composition.
  • a further component i.e., medicament or fine excipient
  • the blending procedure employed herein comprised sandwiching the further component between the two halves of preblend and blend for 10 minutes at 90 rpm using a Turbula T2 blender.
  • Cascade Impaction (Cl) The blends were introduced into a multi-stage cascade impactor by passing a stream of gas over the substrate recess. This allows the blend to be aerosolized and introduced into the impactor.
  • a reduced cascade impactor i.e., stages 3 -
  • each blend was then aerosolized into the cascade impactor at 28.31 min. Referring to Table Til, each data point represents an individual blister. Note: three (3) blisters were employed to demonstrate the variability in performance.
  • the data indicates that different size fines can be employed in conjunction with an aerodynamically light carrier (e.g., porous excipient) to give consistently high FPM performance.
  • an aerodynamically light carrier e.g., porous excipient
  • Blends 3 and 6 were subjected to a preblend. Blends 4 and 5 were not subjected to a preblend. All three components were, however, mixed in a single blending step.
  • blends 9 and 11 were subjected to a preblend, while blends 8 and 10 were not. All three components were, however, mixed in a single blending step.
  • a 100 gm blend was prepared having the composition shown in Table NIII.
  • the data set forth in Table XV indicates that a range of fine excipients can be employed to provide good FPM performance and emitted dose performance.
  • the powder flow properties can be modified through the size/shape or type of fine excipient. Accordingly, powder flow properties can be changed to suit the processes used during the manufacturing process.
  • the stability data indicates that the low density excipient based formulation has significantly better stability in open blisters than the blends typically employed in MDPIs.
  • Examples 27-30 20 gm coarse carrier blends were prepared as shown in Table XNIII.

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EP1487417A4 (en) 2010-03-17
EP1487417A2 (en) 2004-12-22
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US8337816B2 (en) 2012-12-25
JP2005507881A (ja) 2005-03-24
US20040241232A1 (en) 2004-12-02
WO2003024396A3 (en) 2004-09-30

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